Technology

A two-stage crystallization process built around internal energy reuse.

Slipstream’s X-Series architecture combined falling film evaporation, mechanical vapor recompression, condensation, and closed-vessel crystallization to separate industrial wastewater into recovered distillate and a dewatered solids stream—with energy reuse carried through the crystallization process.

Falling Film Evaporation Efficient Stage I vapor generation from a recirculating liquid film
Mechanical Vapor Recompression Compression and reuse of process vapor as thermal energy
Closed-Vessel Crystallization Secondary dewatering with monitored solids handling
Technology Overview

Energy reuse carried beyond evaporation and into crystallization.

The X-Series was designed as a complete wastewater crystallization system. Stage I recovered water and concentrated the feed. Stage II further dewatered the concentrated slurry and prepared the resulting solids for controlled discharge. Vapor from both stages was incorporated into the system’s energy-reuse strategy.

The defining feature of the architecture was the integration of primary evaporation, vapor recompression, condensation, and secondary crystallization within one automated platform.
Process Flow

Five linked steps from feedwater to final outputs.

The treatment sequence was designed to operate continuously through Stage I, with concentrated material periodically transferred to Stage II for further dewatering.

01

Feed

Wastewater enters from a facility holding tank through the integrated feed system.

02

Evaporate

Stage I recirculates the wastewater across the heat-transfer surface and produces vapor.

03

Recompress

The MVR compressor increases the vapor’s temperature and pressure for reuse.

04

Condense

Reused vapor transfers heat and condenses into recovered distilled water.

05

Crystallize

Stage II further dewaters the concentrate and supports solids discharge.

Conceptual Stage I falling film reactor
Stage I Reactor

Primary evaporation, concentration, and distillate recovery.

Stage I received the wastewater, recirculated it through the reactor, and used low-pressure steam and recompressed vapor to raise the liquid to its boiling point. The reactor was designed to operate at low pressure, with a documented maximum operating pressure of approximately 5 psig.

  • Integrated wastewater feed and recirculation
  • Falling film heat-transfer architecture
  • Typical wastewater temperature controlled below approximately 235°F
  • Low-pressure Stage I operation at approximately 5 psig or less
  • Automatic distillate transfer to storage or a process reuse point
  • Automatic concentrate transfer to Stage II at the control setpoint
Mechanical Vapor Recompression

Capturing vapor and returning it to the process as useful heat.

The MVR compressor received low-pressure vapor from the evaporation process and compressed it, raising its pressure and temperature. The compressed vapor could then be routed back into the Stage I heat-transfer cycle rather than being discarded.

4-inch connections Documented vapor inlet and outlet size
1,000 CFM Maximum flow at 80 Hz
5 psig differential Maximum documented pressure rise
1.3:1 ratio Maximum single-stage compression ratio
Mechanical vapor recompression energy flow Low-Pressure Process Vapor Compressed Reusable Vapor Pressure and temperature increased
Heat-Transfer Performance

Scale control supported efficiency; maintainability protected it.

Scaling was the principal technical challenge because deposits on the heat-transfer surfaces reduced the efficiency of thermal energy transfer. Slipstream’s development path focused on preventing or managing that condition rather than excluding difficult wastewater chemistry from the application landscape.

Anti-scaling chemical injection and upstream solids removal protected performance. Accessible heat-transfer surfaces made cleaning and scale removal practical when fouling occurred.
  • Application-specific anti-scaling chemical injection
  • Upstream solids separation when particulate loading warranted it
  • Accessible wetted and heat-transfer surfaces
  • Replaceable heat-transfer components rather than a disposable system architecture
  • Maintenance strategy designed around restoring efficient energy transfer
Stage II Crystallization

Further dewatering with monitored solids handling.

Once Stage I reached its concentration setpoint, the reactor automatically transferred its contents to the Stage II crystallization chamber. Low-pressure steam then continued the evaporation process while an internal rake kept the solids moving.

  • Closed-vessel evaporative crystallization chamber
  • Low-pressure steam supplied to the heat-transfer surfaces
  • Integrated gear motor and 316 stainless rake assembly
  • Weight and process monitoring to determine dewatering progress
  • Controlled solids discharge into a drum, roll-off, supersack, or similar container
  • Stage II vapor returned to Stage I for additional energy reuse

Documented Stage II Operating Logic

Concentrate transfer Automatic
Primary heat source 15 psig steam
Solids agitation Continuous rake
Dewatering indication Weight + pressure
Operator notification HMI + alarm
Discharge method Controlled dump valve
Recovered Outputs

Two manageable product streams instead of one liquid waste stream.

The X-Series separated incoming wastewater into recovered distillate and a concentrated or crystallized solids stream. Output quality and solids consistency varied with operating conditions, while the core architecture was intended to remain broadly applicable across difficult wastewater chemistry.

H₂O

Recovered Distillate

Condensed process vapor was automatically transferred to a holding tank or directly to a facility reuse point. Historical documents describe typical distillate quality below 30 mg/L TDS in one source and below 50 mg/L TDS in another.

S

Dewatered Solids

The Stage II chamber reduced the residual liquid volume and discharged crystallized or semi-dry solids into a customer-selected container for disposal, recycling, or potential material recovery.

Automation and Controls

Sequenced operation with continuous process monitoring.

The X-Series control architecture was designed to verify system readiness, regulate operating parameters, sequence transfers, and notify the operator when intervention was required.

01

PLC and HMI

Allen-Bradley PLC and touchscreen HMI for system operation, setpoints, alarms, and operator interaction.

02

Pressure, Flow, and Level

Pressure regulation, continuous level indication, and flow monitoring with analog instrumentation.

03

Weight and Solids Readiness

Integrated strain-gauge monitoring supported Stage II dewatering control and discharge readiness.

Safety Architecture

Pressure, access, thermal, and electrical safeguards.

Historical process documentation identified multiple mechanical and controls-based safety measures incorporated into the equipment.

Pressure Relief Steam-rated relief valves on pressurized vessels with application-appropriate set pressures.
Directional Safety Valves Actuated inlet piping designed to reduce overflow or liquid release during a power loss.
Guarded Access Locking manual valves and a coded magnetic safety interlock on the Stage II chamber.
Electrical and Thermal Protection Labeled electrical enclosures, insulated hot surfaces, and industrial control components.

The descriptions and values on this page reflect historical Slipstream engineering and marketing documents. Distillate quality, recovery, energy use, operating cost, solids dryness, anti-scaling chemistry, upstream solids management, cleaning frequency, and final materials selection require current engineering review.

Explore the technology as an application, licensing, or acquisition opportunity.

Start a technical discussion about the X-Series architecture, the X-180 platform, and the next phase of commercialization.

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